Upload
others
View
1
Download
0
Embed Size (px)
Citation preview
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 08 Issue: 03 | Mar 2021 www.irjet.net p-ISSN: 2395-0072
© 2021, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 266
Heat Exchangers in Aerospace Applications
Narayan Thakur, Advait Inamdar, Deepak Pal, Akshat Mohite
Narayan Thakur, Mechanical Engineer, AP Shah Institute of Technology, Thane, Maharashtra, India Advait Inamdar, Mechanical Engineer, AP Shah Institute of Technology, Thane, Maharashtra, India
Deepak Pal, Mechanical Engineer, Rajendra Mane College of Engineering and Technology, Ratnagiri, Maharashtra, India
Akshat Mohite,Mechanical Engineer, AP Shah Institute of Technology, Thane, Maharashtra, India
---------------------------------------------------------------------***---------------------------------------------------------------------Abstract - Heat is a form of energy which is transferred
when there is a difference in temperature between two or
more bodies. In some cases transfer of heat energy can be
determined by simply applying the laws of thermodynamics
and fluid mechanics. Heat can be transferred by three
different means, namely, Conduction, Convection and
Radiation. The requirements of thermal management in
aerospace applications are continuously growing, whereas
the weight and volume requirements of the systems remain
constant or shrink. Aerospace systems have high heat flux
requirement and it requires compact, high performance and
light weight equipment with the capacity to withstand low
or no atmospheric pressure. Various experiments and
computational methods have been carried out for
management of heat transfer and its applications in an
aircraft. Although these experiments have not been able to
understand the basic mechanism of thermal convection and
thermal radiation in space applications. Heat exchangers
play a very important role in thermal management of an
aerospace system. This paper introduces numerous
standard applications of heat exchangers in aerospace
systems and presents a few concepts of heat exchangers,
which have been used in aerospace or may be thought about
as promising designs for aerospace industry.
Key Words: Heat, Heat energy, Thermodynamics, Fluid Mechanics, Conduction, Convection, Radiation, Thermal Management, Aerospace, heat flux, Heat exchangers.
1. INTRODUCTION Heat exchangers are equipment being used for transfer of
heat between two or more fluids at different
temperatures. They are widely used in power plants, auto
motives, space heating, refrigeration and air-conditioning
systems, aerospace industry, petrochemical processes and
electronics cooling. In aerospace industry, heat exchangers
are mainly used in three systems: (1) gas turbine cycle, (2)
environmental control system (ECS), and (3) thermal
management of power electronics. Heat exchangers may
be classified in various ways, e.g., based on transfer
processes, surface compactness, construction features,
flow arrangements, and heat transfer mechanisms. Design
and sizing of heat exchangers are generally complicated.
In general, heat transfer, pressure loss, cost, materials,
operating limits, size and weight are important
parameters. Especially for aerospace industry, the weight
and the size of the heat exchanger are most important.
Numerous improvement techniques, for example,
extended surfaces such as the fins, are used in heat
exchangers to enhance the surface area for heat transfer
or the heat transfer coefficient, or both. The aim of
improvement techniques could be to reduce the size of the
heat exchanger for a given function, to increase the
capacity of an existing heat exchanger, or to reduce the
approach temperature difference. Implementation of heat
transfer enhancement techniques in aerospace heat
exchangers might help reduce fuel consumption and the
size of the heat exchanger.
1. APPLICATIONS OF HEAT
EXCHANGERS IN AEROSPACE
2.1. GAS TURBINE CYCLES
Heat exchangers can be implemented in gas turbine cycles
to increase thermal efficiency. For a conventional gas
turbine cycle, the thermal efficiency mainly depends on
the overall pressure ratio and the turbine inlet
temperature. The overall pressure ratio indicates the ratio
of the compressor outlet pressure to the compressor inlet
pressure. The overall pressure ratio and the turbine inlet
temperature are limited by the maximum pressure and
temperature that the turbine blades can withstand. New
materials and innovative cooling concepts for the critical
components can further increase the overall pressure
ratio and the turbine inlet temperature.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 08 Issue: 03 | Mar 2021 www.irjet.net p-ISSN: 2395-0072
© 2021, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 267
A method to improve the overall pressure ratio for a given
compression work is to introduce multistage compression
with intercooling, in which the gas is compressed in stages
and cooled between each stage by passing the gas through
a heat exchanger called an intercooler. Gas turbine engines
in aerospace industry require high overall pressure ratio.
To achieve higher pressure ratio, the compressor is
divided into a low pressure compressor (LPC) and a high
pressure compressor (HPC). This is done to introduce an
intercooler between LPC and HPC. The compressed gas
has a relatively higher temperature at the outlet of LPC. By
using a crossflow or counterflow air-to-air heat exchanger,
with compressed air flowing on one side and low-
temperature ram air flowing on the other side, the
compressed air can be cooled before entering the HPC. The
steady-flow compression work or the pressure ratio for a
given compression work is proportional to the specific
volume of the compressed air [8]. The intercooler
decreases the temperature and hence decreases the
specific volume of the compressed air, which improves the
thermodynamic cycle efficiency. In gas turbine engines,
the temperature of the exhaust gases leaving the turbine is
often considerably higher than that of the air leaving the
HPC. A regenerator or a recuperator, i.e. a crossflow or
counterflow heat exchanger, can be incorporated to
transfer heat from the hot exhaust gases to the
compressed air. Accordingly, the thermal efficiency
increases because the portion of the energy of the exhaust
gases that is supposed to be rejected to the surroundings
is recovered to preheat the air entering the combustion
chamber. The recuperator is more advantageous when an
intercooler is used because a greater potential for
recuperation exists. A recuperator is not effective, for
highoverall pressure ratios, especially considering its cost,
size and weight. Fig 1 shows a conceptual sketch that
compares the thermal efficiencies of different gas turbine
cycles with the overall pressure ratios. In general, the
intercooled and recuperated gas turbine cycle is effective
at relatively low overall pressure ratios, e.g. less than 30.
The intercooled gas turbine cycle without recuperation is
only effective at very high overall pressure ratios. Fig 2
illustrates an intercooled and recuperated gas turbine
cycle.
Figure.1 Thermal efficiency versus overall pressure ratio
for different gas turbine cycles. Adapted from Sieber J,
Overview NEWAC (new aero engine core concepts); April
2009.
Figure.2 Intercooled and recuperated gas turbine cycle.
LPC, low-pressure compressor; HPC, high-pressure
compressor; Com, compressor; HPT, high-pressure
turbine; LPT, low-pressure turbine Adapted from Sieber J,
Overview NEWAC (new aero engine core concepts); April
2009.
In addition, precoolers, such as cryogenic fuel-cooled air
heat exchangers, that immediately downstream the air
intake to precool the air entering the engine can be used
for high-speed jet engines to save fuel consumption for a
given overall pressure ratio or to increase the overall
pressure ratio for a given compression work. Besides,
modern gas turbine engines operate at turbine inlet air
temperature levels that are beyond the material maximum
temperature. Hence, hot engine components such as the
turbine blades must be cooled to assure their structural
integrity. Typically the turbine blades are cooled by bleed
air from the compressor, which, although cooler than the
turbine, has been already heated up by the work done on
it by the compressor [8]. Engine bleed reduces thrust and
increases fuel burn. The effect is a function of the mass
flow rate of the bleed air. If a heat exchanger is used to
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 08 Issue: 03 | Mar 2021 www.irjet.net p-ISSN: 2395-0072
© 2021, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 268
cool the bleed air before its introduction for blade cooling,
the amount of bleed air required by the blade cooling can
be reduced, which results in an improved engine
performance with a consequent reduction in specific fuel
consumption (the rate of fuel consumption per unit of
power output). Such a heat exchanger might be a fuel-to-
air heat exchanger. The relatively hot bleed air can be
cooled by the cool engine fuel. On one hand, the cooling
capacity of the bleed air increases as its temperature is
decreased. On the other hand, the energy extracted by the
fuel is reintroduced into the propulsive cycle as the heated
fuel is burned in the combustor.
1.2 ENVIRONMENTAL CONTROL SYSTEM
The ECS is employed in aerospace vehicles such as large
commercial aircraft to provide comfortable flight
conditions for passengers. There are two kinds of air-
conditioning systems on an aircraft: air cycle air-
conditioning and vapor cycle refrigeration system. For air
cycle air-conditioning, the source of air used by the ECS is
typically bleed air from the gas turbine compressor, with a
relatively high pressure and temperature. The hot bleed
air must first be cooled to an acceptable temperature
before entering into the passenger cabin. This is
performed using an air-conditioning package that is
composed of several units, including a number of heat
exchangers cooled by ambient ram air. As shown in Fig. 3
the hot bleed air from the engine compressor is metered
through a bleed air valve and then cooled by the primary
heat exchanger. Then the air passes to the air cycle
machine for pressure adjustment and finally into the
secondary heat exchanger for temperature adjustment
before entering the cabin. The primary and secondary heat
exchangers shown in Fig.3 are air-to-air heat exchangers.
A vapor cycle refrigeration system, in which the
refrigerant undergoes phase changes, is basically the same
refrigeration cycle that is used in home air conditioners.
The vapor cycle refrigeration system is a closed system
used for transferring heat from inside the cabin to outside
the cabin. Heat exchangers such as evaporators and
condensers are important devices in the refrigeration
cycle. Specifically the liquid refrigerant decreases its
pressure by passing through a thermal expansion valve
before entering the evaporator. The liquid refrigerant in
the evaporator changes into vapor, absorbing the heat
energy from the cabin air. The vapor is then compressed
and becomes hot. The hot vapor refrigerant transfers its
heat energy to the outside ram air in a condenser and thus
the refrigerant condenses back into liquid to repeat the
cycle. Therefore, the warm cabin air is constantly replaced
or mixed with cool air in the aircraft cabin to maintain a
comfortable temperature. An example of a vapor cycle
refrigeration system is shown in Fig. 4.
Figure 3 A schematic of an Airbus air-conditioning system
[10]. HEX, heat exchanger.
Figure 4 A vapor cycle refrigeration system.
1.3 THERMAL MANAGEMENT
The trend to pack current and future aerospace and
military platforms with power-hungry, heat-generating
electronic components and systems drives the need for
efficient, effective, compact, and lightweight thermal
management systems. Shrinking electronics packaging and
high-density integration of power electronics to enable
more power and functionality in a small unit, coupled with
the extremes of military and aerospace environments,
constantly place ever-increasing demands on precise and
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 08 Issue: 03 | Mar 2021 www.irjet.net p-ISSN: 2395-0072
© 2021, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 269
smart thermal management solutions to maintain junction
temperatures below levels that degrade performance. The
temperature of the components can be maintained at a
safe level by air cooling for low-heat-flux components. As
the heat flux increases, the limits of air cooling technology
are being approached, i.e., forced air heat sinks have
become significantly larger, more expensive, and more
complex. Liquid cooling is promising to provide the
needed level of thermal performance, with an increase in
energy efficiency compared to traditional air cooling. The
liquid must pass through the heat sources to carry away
the heat, resulting in a temperature increase in the liquid.
Then the liquid passes through a liquid-to-air heat
exchanger, such as a plate-fin heat exchanger (PFHE), to
transfer the stored heat to the air. An important
component for liquid cooling is the cold plate. The cold
plate must be able to dissipate the waste heat efficiently
within a relatively small unit. Fig.5 shows examples of cold
plates, namely, the tube liquid cold plate and the
powdered metal cold plate [11], with the former suitable
for low heat fluxes and the latter for high heat fluxes. Cold
plates with embedded microchannels are promising to
dissipate high heat fluxes. In many cases, heat pipes are
embedded in cold plates to increase the effective thermal
conductivity of the cold plates. Basically the cold plates
should be designed by conforming to the heat-generating
components. Besides, the cold plates should be optimized
to augment the thermal performance while maintaining a
relatively low pressure drop penalty by properly
designing, e.g., the liquid flow passages and manifold
distributions inside the cold plates. A liquid cooling
concept is sketched in Fig.6.
Figure 5 Cold plate examples: (a) a tube liquid cold plate
and (b) a powdered metal cold plate.
For ultrahigh heat flux components such as converters or
densely packed computing devices with heat fluxes
greater than 100 W/cm2, liquid cooling might not be
sufficient enough to cool the heat-generating components
with certain form factors. Besides, similar to air cooling,
liquid cooling cannot provide relatively uniform cooling as
the liquid temperature increases along the cooling path.
One way of providing an efficient cooling system for high-
power-density electronic devices is by using an
evaporative cooling circuit. This circuit brings a liquid into
thermal contact with the heat-generating components via
an evaporating unit to effectively remove heat by utilizing
the latent heat of the working fluids and at the same time
to maintain a relatively uniform temperature distribution.
Compared to air cooling and single-phase liquid cooling,
microchannel evaporative cooling has a low pumping
power requirement relative to the quantity of heat to be
removed [12]. At the same total flow rates, the pressure
drop in evaporative microchannels is much higher than
that for single-phase liquid flow in conventional channels.
However, to dissipate the same amount of heat, much less
liquid is required in microchannel evaporative cooling
than that in single-phase liquid cooling. Fig.7 shows an
evaporative cooling loop with a pump, a cold plate
evaporator, an air-cooled condenser, and a reservoir. It
has been stated that such an evaporative cooling system
with refrigerant R134a as the working fluid can provide
twice the cooling capacity in half the size or in a size less
than that of air- or water-cooling systems [13].
Figure 6 A concept of a liquid cooling solution.
Besides, the temperature of lubricating oil needs to be
controlled. The excessive heat caused by friction in devices
such as gearboxes and compressors increases the
lubricant oil temperature. As the oil viscosity decreases
with increment in temperature, the lubricant oil film
becomes thinner and collapses, which in turn causes more
friction and heat. Fuel or ambient ram air can be used as
working fluids in fuel-cooled oil cooler or air-cooled oil
cooler to cool the lubricants.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 08 Issue: 03 | Mar 2021 www.irjet.net p-ISSN: 2395-0072
© 2021, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 270
Figure 7 An exemplified evaporative cooling system.
3. GENERAL DESIGN CONSIDERATIONS FOR
AEROSPACE HEAT EXCHANGERS
The typical features of aerospace heat exchangers are
briefly listed below.
• Compactness and lightweight: Compact heat exchangers
are promising because of the limited space available for
heat transfer in aerospace industry. Light materials such
as aluminum alloy and metal foam might be preferred if
the operating pressure and temperature are less than the
maximum allowable pressure and temperature of the
materials.
• Relatively high temperature and pressure for some
aerospace heat exchangers such as recuperators:
Compressed air leaving the HPC flows on one side of the
recuperator and the exhaust gas exits from the turbine
flows on the other side. For example, for an overall
pressure ratio of 50, the compressed air leaving the HPC
has a pressure of 50 bar and a temperature up to 1000 K.
The materials for high-temperature heat exchangers
should be able to maintain structural integrity to cope
with large temperature differences.
• High effectiveness and minimum pressure loss: The heat-
exchanging surfaces and flow paths should be designed in
such a way to give a high thermal conductance with a
minimum pressure loss. Besides, the bypass duct and the
inlet and outlet ducts to and from the heat exchangers
need to be arranged properly to minimize momentum
pressure losses.
4. TYPES OF HEAT EXCHANGERS
4.1 PLATE-FIN HEAT EXCHANGERS
A PFHE consists of flat plates and finned chambers to
transfer heat between fluids. PFHE is often categorized as
a compact heat exchanger with a relatively high heat
transfer surface area to volume ratio. In aerospace
industry, aluminum alloy PFHEs have been used for 50
years for their compactness and lightweight properties.
Most commonly this heat exchanger type is for gas-to-gas
heat exchange. Various fin geometries such as triangular,
rectangular, wavy, louvered, perforated, serrated, or the
so-called offset strip fins are used to separate the plates
and create the flow channels. The common fin thickness
ranges from 0.046 to 0.20 mm and the fin height ranges
from 2 to 20 mm.
Figure 9. Types of fin geometries: (a) rectangular fin, (b)
wavy fin, (c) offset strip fin, and (d) louvered fin.
4.2 PRINTED CIRCUIT HEAT EXCHANGERS
The concept of PCHEs was first invented in the early
1980s at the University of Sydney in Australia. It has been
commercially manufactured by Heatric Ltd in the United
Kingdom since 1985. A brief introduction of PCHE is given
in Reay et al. [4]. The PCHE derives its name from the
procedure used to manufacture the plates that form the
core of the heat exchanger; the fluid flow passages are
produced by chemical milling, a technique similar to that
used to manufacture printed circuit boards in the
electronics industry. A benefit of this design is the
flexibility it affords in terms of flow passage geometry. The
fluid flow passages for PCHE have approximately a
semicircular cross section. Channel depths and channel
widths are typically in the range 0.5–2.0 mm and 0.5–5.0
mm, respectively, and may be larger for some streams.
PCHEs are highly compact because of their high surface
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 08 Issue: 03 | Mar 2021 www.irjet.net p-ISSN: 2395-0072
© 2021, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 271
area-to-volume ratios (>2500 m2/m3) [15]. A PCHE is a
high-efficiency plate-type compact heat exchanger, which
is typically four to six times smaller and lighter than a
shell-and-tube heat exchanger of equivalent performance.
Figure 10. A diffused PCHE
4.3 MICRO HEAT EXCHANGERS
Micro- and miniscale heat exchangers (μHEXs) are heat
exchangers in which at least one fluid flows in lateral
confinements such as channels or small cavities with
dimensions less than around 1 mm in size. Some PFHEs
and PCHEs can also be categorized as μHEXs. Typically, the
fluid flows through a cavity that is called a microchannel.
This process intensification technology exploits heat
transfer enhancement resulting from structurally
constrained fluid streams in microchannels, which reduces
the thermal resistance considerably. Micro heat
exchangers have been demonstrated with high heat
transfer coefficients, approximately one order of
magnitude higher than the typical values of conventional
heat exchangers. Therefore, as a typical miniaturized
process device, micro heat exchangers have attracted
widespread applications because of their high thermal
performance, compactness, small size, and lightweight
[20], with the aim of process intensification. Micro heat
exchangers are used in diverse energy and process
applications such as electronics cooling, automotive and
aerospace industries, chemical process intensification,
refrigeration and cryogenic systems, and fuel cells. Micro
heat exchangers have many advantages over conventional
heat exchangers. First, in the scaling down from macro- to
microscale, the volume decreases with the third power of
the characteristic linear dimensions, whereas the surface
area only decreases with the second power. Therefore,
micro heat exchangers have relatively larger surface area-
to-volume ratios that enable higher heat transfer rates
than conventional heat exchangers. Second, fast fluid
acceleration and close proximity of the bulk fluid to the
wall surface in μHEXs give high heat transfer coefficients.
For single-phase fully developed internal laminar flow, a
constant Nusselt number (Nu = hdh/k) implies that the
single-phase heat transfer coefficient increases as the
hydraulic diameter decreases. In addition, compactness
and high heat-flux dissipation are required as the scale of
the devices decreases, whereas the power density
increases. Micro heat exchangers are expected to manage
the high heat-flux dissipation for miniaturized devices to
guarantee the reliability and safety during operation.
Figure 11. Examples of micro heat exchangers: (a)
ceramic micro heat exchanger [24] and (b) 3D-printed
heat exchanger by Sustainable Engine Systems Ltd. [4].
5. OTHER AEROSPACE HEAT EXCHANGERS
5.1 PRIMARY SURFACE HEAT EXCHANGERS
Primary surface heat exchangers refer to heat exchangers
wherein substantially all the material that conduct heat
between two media comprises the walls separating the
two media. This type of heat exchangers primarily consists
of plates or sheets and have no separate or additional
internal members, such as fins, so that the exchanger is
constructed of plates or sheets, each side of which is in
contact with a different fluid, and heat transfer occurs
substantially and directly between the plates and the fluid.
In contrast, extended surface heat exchangers, or
secondary surface heat exchangers, contain a substantial
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 08 Issue: 03 | Mar 2021 www.irjet.net p-ISSN: 2395-0072
© 2021, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 272
amount of material in the form of fins, which do not
separate the media. The PFHE and micro heat exchanger
are mostly extended surface heat exchangers. The main
attributes of primary surface heat exchangers are that the
surface geometry is 100% effective (no fins) and sealing
can be accomplished by welding without the need for an
expensive and time-consuming high-temperature furnace
brazing operation. Primary surface heat exchangers can be
used as intercoolers and recuperators in the aerospace
industry.
5.2 HEAT PIPE HEAT EXCHANGER
Heat pipes of various capillary wick structures are
attractive in the area of spacecraft cooling and
temperature stabilization because of their lightweight,
zero maintenance, and reliability. A heat pipe consists of
an evaporation zone, an adiabatic zone, and a
condensation zone. Liquid in contact with the evaporation
zone turns into vapor by absorbing heat, and vapor then
travels along the heat pipe to the condensation zone and
condenses back into liquid, releasing the latent heat. The
liquid then returns to the evaporation zone through
capillary forces or other external forces. Loop heat pipes
and micro/miniature heat pipes are promising types
suitable for cooling solutions. Micro heat pipes are heat
pipes with a height less than about 1 mm. Micro and
miniature heat pipes are able to dissipate high heat fluxes
up to 100 W/cm2 [29]. A major advantage of heat pipes is
that no external power is required. For high heat fluxes,
heat pipes need a relatively larger area for heat dissipation
from the heat pipe condensation zone to the environment,
which might be a concern because of the limited space in
aerospace. The depth of the micro heat pipe is less than
1.0 mm. The width and the length of the evaporation zone
depend on the form factor of the electronic components.
The length of the condensation zone can be designed by
the required dissipated heat and the cooling mode of the
external heat sink.
Figure 12. A flat micro heat pipe.
6. HEAT EXCHANGERS USING NEW MATERIALS
6.1 FOAM MATERIALS
Light materials are preferred in the manufacturing of
aerospace heat exchangers to save fuel consumption.
Aluminum alloy heat exchangers such as aluminum alloy
PFHEs are common in the aerospace industry. Foam
materials such as open-cell porous metallic foams and
graphite foams have received increased attention for use
in commercial heat exchangers because of their
lightweight, improved thermal performance, high
compactness, attractive flexibility to be formed in complex
shapes, good stiffness/strength properties, and low cost
via the metal sintering route for mass production, as well
as because some materials can be used at high
temperatures up to 1200 K. Because of the
interconnection of pores and tortuosity of open-cell foams,
fluid mixing and convection heat transfer are greatly
enhanced. The key parameters that influence the
thermohydraulic performance of foams are porosity, pore
density (pores per inch), mean pore diameter, surface
area-to-volume ratio, effective thermal conductivity, and
permeability. The pertinent correlations for flow and
thermal transport in metal foam heat exchangers were
categorized in Ref. [30] Graphite foam is attractive, as the
density of graphite foam ranges from 200 to 600 kg/m3,
which is about 20% of that of aluminum. However, the
tensile strength of graphite foam is much less than that of
metal foam. The weak mechanical properties of graphite
foam block its development as a heat exchanger. Adding
more material into the graphite foam or changing the
fabrication process might improve the mechanical
properties of the foam [31]. The major disadvantage of
open-cell foams is the relatively high pressure drop
penalty, as pointed out by Muley et al. [32]. Besides, at
present, foam heat exchangers are not suitable for high-
pressure conditions, as the maximum pressure for foam
heat exchangers is relatively low.
6.2 CERAMIC MATERIALS
The two main advantages of using ceramic materials and
ceramic matrix composites (CMCs) in heat exchanger
construction over traditional metallic materials are their
temperature resistance and corrosion resistance. Ceramics
and CMCs are now used in rocket nozzles and jet engines,
heat shields for space vehicles, aircraft brakes, gas
turbines for power plants, fusion reactor walls, heat
treatment furnaces, heat recovery systems, etc. Major
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 08 Issue: 03 | Mar 2021 www.irjet.net p-ISSN: 2395-0072
© 2021, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 273
obstacles preventing the wide use of ceramics include
ceramic-metallic mechanical sealing, manufacturing costs
and methods, and their brittleness in tension. The most
commonly used CMCs are non-oxide CMCs, i.e.,
carbon/carbon, carbon/silicon carbide, and silicon
carbide/silicon carbide. At present, various heat
exchangers, such as PFHEs, micro heat exchangers, and
primary surface heat exchangers, can be manufactured by
ceramics. Ceramic recuperators and intercoolers can be
used to improve the gas turbine cycle efficiency.
Figure 13. (a) Open-cell metal foam and (b) a foam heat exchanger [32].
7. CONCLUSION
Aerospace heat exchangers are mainly used in gas turbine
cycles, ECSs, and thermal management of various
aerospace systems. The applications of aerospace heat
exchangers are discussed. The main features are listed for
aerospace heat exchangers. This paper also illustrates
various typical compact heat exchangers including PFHEs,
micro heat exchangers, PCHEs, primary surface heat
exchangers, and heat pipes, which are favorable to provide
efficient heat transfer and cooling in the aerospace
industry.
REFERENCES
[1]Sundén B. Introduction to heat transfer. Southampton:
WIT Press; 2012.
[2] Shah R.K, Sekulić D.P. Fundamentals of heat exchanger
design. John Wiley & Sons, Inc; 2003.
[3] Wang L, Sundén B, Manglik R.M. Plate heat exchangers:
design, applications and performance. WIT Press; 2007.
[4] Reay D, Ramshaw C, Harvey A. Process intersification:
engineering for efficiency, sustainability and flexibility.
Oxford: Butterworth-Heinemann; 2013.
[5] Bergles A.E. ExHFT for fourth generation heat transfer
technology. Exp Therm Fluid Sci. 2002;26(2):335–344.
[6] Webb R.L, Kim N.H. Principles of enhanced heat
transfer. Taylor & Francis Group; 2005.
[7] European commission, flightpath 2050 Europe's vision
for aviation. 2011.
[8] Yunus A.C, Michael A.B. Thermodynamics: an
engineering approach. New York: McGraw-Hill; 2006.
[9] Sieber J. Overview NEWAC (new aero engine core
concepts). April 2009.
[10] Wright S, Andrews G, Sabir H. A review of heat
exchanger fouling in the context of aircraft air-
conditioning systems, and the potential for electrostatic
filtering. Appl Therm Eng. 2009;29(13):2596–2609.
[11] North M.T, Cho W.L. High heat flux liquid-cooled
porous metal heat sink. In: Proceedings of Interpack '03,
ASME paper IPACK2003-35320, Kaanapali, HI. 2003. .
[12]Marcinichen J.B, Olivier J.A, Thome J.R. Reasons to use
two-phase refrigerant cooling. Electronics Cooling
Magazine; March 2011:22–27.
[13] Thompson D. Cool system, hot results. Wind systems
magazine; February 2010:40–43.
[14] Strumpf H, Mirza Z. Development of a microchannel
heat exchanger for aerospace applications. In: ASME 2012
10th International Conference on Nanochannels,
Microchannels, and Minichannels collocated with the ASME
2012 Heat Transfer Summer Conference and the ASME 2012
Fluids Engineering Division Summer Meeting. American
Society of Mechanical Engineers; 2012:459–467.
[15] Focke W.W, Zachariades J, Olivier I. The effect of the
corrugation inclination angle on the thermohydraulic
performance of plate heat exchangers. Int J Heat Mass
Transf. 1985;28(8):1469–1479.
[16]Mylavarapu S.K, Sun X, Christensen R.N, Unocic R.R,
Glosup R.E, Patterson M.W. Fabrication and design aspects
of high-temperature compact diffusion bonded heat
exchangers. Nuc Eng Des. 2012;249:49–56.
International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 08 Issue: 03 | Mar 2021 www.irjet.net p-ISSN: 2395-0072
© 2021, IRJET | Impact Factor value: 7.529 | ISO 9001:2008 Certified Journal | Page 274
[17] Nicholas M.G. Joining processes: introduction to
brazing and diffusion bonding. Springer; 1998.
[18] Tsuzuki N, Kato Y, Ishiduka T. High performance
printed circuit heat exchanger. Appl Therm Eng.
2007;27(10):1702–1707.
[19]Kim D.E, Kim M.H, Cha J.E, Kim S.O. Numerical
investigation on thermal–hydraulic performance of new
printed circuit heat exchanger model. Nuc Eng Des.
2008;238(12):3269–3276.
[20] Dixit T, Ghosh I. Review of micro- and Mini-channel
heat sinks and heat exchangers for single phase fluids.
Renew Sustain Energy Rev. 2015;41:1298–1311.
[21] Tuckerman D.B, Pease R.F.W. High-performance heat
sinking for VLSI. IEEE Electron Device Lett. 1981;2:126–
129.
[22] Wu Z, Sundén B. On further enhancement of single-
phase and flow Boiling heat transfer in
micro/Minichannels. Renew Sustain Energy Rev.
2014;40:11–27
.[23] Sundén B, Wu Z. Advanced heat exchangers for clean
and sustainable technology. In: Yan J, ed. Handbook of
clean energy systems. John Wiley & Sons; 2015.
[24]Alm B, Imke U, Knitter R, Schygulla U, Zimmermann S.
Testing and Simulation of ceramic micro heat exchangers.
Chem Eng J. 2008;135:S179–S184.
[25] Morini G.L. Scaling effects for liquid flows in
microchannels. Heat Transf Eng. 2006;27:64–73.
[26] Maranzana G, Perry I, Maillet D. Mini-and micro-
channels: influence of axial conduction in the walls. Int J
Heat Mass Transf. 2004;47:3993–4004.
[27] Nacke R, Northcutt B, Mudawar I. Theory and
experimental validation of cross-flow micro-channel heat
exchanger module with reference to high Mach aircraft gas
turbine engines. Int J Heat Mass Transf. 2011;54(5):1224–
1235.
[28] Baker N. Intercooled engine and integration, European
Workshop on new aero engine concepts, Munich. June 30–
July 1, 2010.
[29] Wang Y, Peterson G.P. Investigation of a novel flat
heat pipe. ASME J Heat Transf. 2005;127(2):165–170.
[30] Mahjoob S, Vafai K. A synthesis of fluid and thermal
transport models for metal foam heat exchangers. Int J
Heat Mass Transf. 2008;51(15):3701–3711.
[31]Lin W.M, Sundén B, Yuan J.L. A performance analysis
of porous graphite foam heat exchangers in vehicles. Appl
Therm Eng. 2013;50(1):1201–1210.
[32]Muley A, Kiser C, Sundén B, Shah R.K. Foam heat
exchangers: a technology assessment. Heat Transf Eng.
2012;33(1):42–51.
[33] Rishmany J, Mabru C, Chieragatti R, Rezaï Aria F.
Simplified modelling of the behaviour of 3D-periodic
structures such as aircraft heat exchangers. Int J Mech Sci.
2008;50(6):1114–1122. .
[34] Ito Y, Nagasaki T. Suggestion of intercooled and
recuperated jet engine using already equipped
components as heat exchangers. In: 47th
AIAA/ASME/SAE/ASEE Joint Propusion Conference &
exhibit, San Diego, California. 2011.
[35]Doo J.H, Ha M.Y, Min J.K, Stieger R, Rolt A, Son C. An
investigation of cross-corrugated heat exchanger primary
surfaces for advanced intercooled-cycle aero engines
(Part-I: novel geometry of primary surface). Int J Heat
Mass Transf. 2012;55(19–20):5256–5267.
[36] Shukla K.N. Heat pipe for aerospace applications—an
Overview. J Electron Cool Therm Control. 2015;5:1–14.
[37]Oliveira J.L.G, Tecchio C, Paiva K.V, Mantelli M.B.H,
Gandolfi R, Ribeiro L.G.S. In-flight testing of loop
thermosyphons for aircraft cooling. Appl Therm Eng.
2016;98:144–156.
[38]Musto M, Bianco N, Rotondo G, Toscano F, Pezzella G.
A Simplified methodology to simulate a heat exchanger in
an Aircraft's oil cooler by means of a porous media model.
Appl Therm Eng. 2016;94:836–845.